Operation and maintenance of anaerobic reactor during shutdown and production reduction period and method for disposal of excess sludge
An anaerobic reactor and excess sludge technology, applied in biological sludge treatment, anaerobic digestion treatment, chemical instruments and methods, etc., can solve the problems of economic loss, large sludge disposal costs, acidification of anaerobic reactors, etc. , to achieve strong promotion and application prospects, enhance overall usability, and improve the effect of COD
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Embodiment 1
[0019] The operation and maintenance of the anaerobic reactor in this embodiment and the method for the disposal of excess sludge during the period of production shutdown and production reduction are carried out according to the following steps:
[0020] 1. Set the water flow rate to 10m 3 / h of water that meets the "Integrated Wastewater Discharge Standard" is sent to the hydrolytic acidification tank of the anaerobic reactor;
[0021] 2. Stop the operation of all stirring equipment in the hydrolytic acidification tank to ensure that only the force generated by the influent water in the hydrolysis acidification tank;
[0022] 3. Transport the excess sludge to the hydrolytic acidification tank, and keep the hydrolytic acidification tank in a static state or a state where the remaining sludge cannot be taken out;
[0023] 4. The sewage in the hydrolytic acidification tank is hydrolyzed by the anoxic sludge, and then transported to the anaerobic reactor.
Embodiment 2
[0025] The operation and maintenance of the anaerobic reactor in this embodiment and the method for the disposal of excess sludge during the period of production shutdown and production reduction are carried out according to the following steps:
[0026] 1. Set the water flow rate to 30m 3 The COD content per hour is lower than 1000mg / L and sent to the hydrolytic acidification tank of the anaerobic reactor;
[0027] 2. Stop the operation of all stirring equipment in the hydrolytic acidification tank to ensure that only the force generated by the influent water in the hydrolysis acidification tank;
[0028] 3. Transport the excess sludge to the hydrolytic acidification tank, and keep the hydrolytic acidification tank in a static state or a state where the remaining sludge cannot be taken out;
[0029] 4. After the sewage in the hydrolysis acidification tank is hydrolyzed through the sludge, it is then transported to the anaerobic reactor.
Embodiment 3
[0031] The operation and maintenance of the anaerobic reactor in this embodiment and the method for the disposal of excess sludge during the period of production shutdown and production reduction are carried out according to the following steps:
[0032] 1. Set the water flow rate to 50m 3 The COD content per hour is lower than 1000mg / L and sent to the hydrolytic acidification tank of the anaerobic reactor;
[0033] 2. Stop the operation of all stirring equipment in the hydrolytic acidification tank to ensure that only the force generated by the influent water in the hydrolysis acidification tank;
[0034] 3. Transport the excess sludge to the hydrolytic acidification tank, and keep the hydrolytic acidification tank in a static state or a state where the remaining sludge cannot be taken out;
[0035] 4. After the sewage in the hydrolysis acidification tank is hydrolyzed through the sludge, it is then transported to the anaerobic reactor.
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